MCP๋กœ ์—ฐ๊ฒฐ โ†’

๊ณ„์‚ฐ ์ž…๋ ฅ

๊ณต์‹

๊ด‘๊ณ 

๊ฒฐ๊ณผ

๋ˆ„์…€ ์ˆ˜
16.6667
๋ฌด์ฐจ์›
์—ด์ „๋‹ฌ ๊ณ„์ˆ˜ h 100 W/mยฒยทK
ํŠน์„ฑ ๊ธธ์ด L 0.1 m
์—ด์ „๋„์œจ k 0.6 W/mยทK

๋ˆ„์…€ ์ˆ˜๋ž€?

๋ˆ„์…€ ์ˆ˜(Nu)๋Š” ์—ด์ „๋‹ฌ ๋ถ„์•ผ์—์„œ ์‚ฌ์šฉ๋˜๋Š” ๋ฌด์ฐจ์› ์ˆ˜๋กœ, ์œ ์ฒด ๊ฒฝ๊ณ„์ธต์„ ๊ฐ€๋กœ์ง€๋ฅด๋Š” ์—ด์ „๋‹ฌ์—์„œ ๋Œ€๋ฅ˜์™€ ์ˆœ์ˆ˜ ์ „๋„์˜ ๋น„์œจ์„ ๋‚˜ํƒ€๋ƒ…๋‹ˆ๋‹ค. \(\text{Nu} = 1\)์€ ์ˆœ์ˆ˜ ์ „๋„์— ์˜ํ•œ ์—ด์ „๋‹ฌ(์ •์ง€๋œ ์œ ์ฒด์—์„œ ์ „ํ˜•์ ์œผ๋กœ ๋‚˜ํƒ€๋‚จ)์„ ์˜๋ฏธํ•˜๋ฉฐ, ๊ฐ’์ด ์ปค์งˆ์ˆ˜๋ก ๋Œ€๋ฅ˜๊ฐ€ ๊ทธ๋งŒํผ ํšจ๊ณผ์ ์œผ๋กœ ์ผ์–ด๋‚˜๊ณ  ์žˆ์Œ์„ ๋œปํ•ฉ๋‹ˆ๋‹ค. ๋…์ผ ์—”์ง€๋‹ˆ์–ด ๋นŒํ—ฌ๋ฆ„ ๋ˆ„์…€(Wilhelm Nusselt)์˜ ์ด๋ฆ„์—์„œ ๋”ฐ์™”์œผ๋ฉฐ, ์—ด๊ตํ™˜๊ธฐยท์ „์ž๊ธฐ๊ธฐ ๋ƒ‰๊ฐยทHVAC(๋ƒ‰๋‚œ๋ฐฉ ๊ณต์กฐ) ์‹œ์Šคํ…œ ์„ค๊ณ„์—์„œ ํ•ต์‹ฌ์ ์ธ ์—ญํ• ์„ ํ•ฉ๋‹ˆ๋‹ค.

Diagram comparing heat conduction across a fluid layer versus convection at a surface, illustrating the Nusselt number ratio
The Nusselt number compares convective to conductive heat transfer across a fluid boundary layer.

๊ณ„์‚ฐ๊ธฐ ์‚ฌ์šฉ ๋ฐฉ๋ฒ•

์„ธ ๊ฐ€์ง€ ๊ฐ’์„ ์ž…๋ ฅํ•˜์„ธ์š”: ๋Œ€๋ฅ˜ ์—ด์ „๋‹ฌ ๊ณ„์ˆ˜ h(W/mยฒยทK), ํŠน์„ฑ ๊ธธ์ด L(m) โ€” ํ”ํžˆ ์ง๊ฒฝ, ํ‰ํŒ ๊ธธ์ด, ๋˜๋Š” ์ˆ˜๋ ฅ ์ง๊ฒฝ์„ ์‚ฌ์šฉํ•ฉ๋‹ˆ๋‹ค โ€” ๊ทธ๋ฆฌ๊ณ  ์œ ์ฒด์˜ ์—ด์ „๋„์œจ k(W/mยทK)์ž…๋‹ˆ๋‹ค. ์ž…๋ ฅํ•˜๋ฉด ๋ฌด์ฐจ์› ๋ˆ„์…€ ์ˆ˜๊ฐ€ ์ฆ‰์‹œ ๊ณ„์‚ฐ๋ฉ๋‹ˆ๋‹ค.

๊ณต์‹ ํ’€์ด

๋ˆ„์…€ ์ˆ˜๋ฅผ ์ •์˜ํ•˜๋Š” ์‹์€ ๋‹ค์Œ๊ณผ ๊ฐ™์Šต๋‹ˆ๋‹ค:

$$\text{Nu} = \frac{\text{h} \cdot \text{L}}{\text{k}}$$

์—ฌ๊ธฐ์„œ h๋Š” ํ‘œ๋ฉด๊ณผ ํ๋ฅด๋Š” ์œ ์ฒด ์‚ฌ์ด์—์„œ ์—ด์ด ์–ผ๋งˆ๋‚˜ ์ž˜ ์ด๋™ํ•˜๋Š”์ง€๋ฅผ, L์€ ๊ด€๋ จ๋œ ๊ธฐํ•˜ํ•™์  ์ฒ™๋„๋ฅผ, k๋Š” ์œ ์ฒด๊ฐ€ ์—ด์„ ์ „๋„ํ•˜๋Š” ๋Šฅ๋ ฅ์„ ๋‚˜ํƒ€๋ƒ…๋‹ˆ๋‹ค. ์„ธ ๋ณ€์ˆ˜์˜ ๋‹จ์œ„๊ฐ€ ์„œ๋กœ ์ƒ์‡„๋˜๊ธฐ ๋•Œ๋ฌธ์— ๊ฒฐ๊ณผ๋Š” ๋ฌด์ฐจ์›์ด ๋˜๋ฉฐ, ๋•๋ถ„์— ํ˜•์ƒ์ด๋‚˜ ์œ ์ฒด๊ฐ€ ๋‹ฌ๋ผ๋„ ์„œ๋กœ ๋น„๊ตํ•  ์ˆ˜ ์žˆ์Šต๋‹ˆ๋‹ค.

Flat schematic showing the three variables of the Nusselt number formula: heat transfer coefficient, characteristic length, and thermal conductivity
The three inputs of Nu = hL/k: surface heat transfer coefficient h, characteristic length L, and fluid conductivity k.

๊ณ„์‚ฐ ์˜ˆ์‹œ

๋ฌผ์ด ์–ด๋–ค ํ‘œ๋ฉด ์œ„๋ฅผ ํ๋ฅด๊ณ  ์žˆ๊ณ  \(h = 500\ \text{W/m}^2\cdot\text{K}\), ํŠน์„ฑ ๊ธธ์ด \(L = 0.05\ \text{m}\), ๋ฌผ์˜ ์—ด์ „๋„์œจ \(k = 0.6\ \text{W/m}\cdot\text{K}\)๋ผ๊ณ  ๊ฐ€์ •ํ•ด ๋ด…์‹œ๋‹ค. ๊ทธ๋Ÿฌ๋ฉด ๋‹ค์Œ๊ณผ ๊ฐ™์ด ๋ฉ๋‹ˆ๋‹ค:

$$\text{Nu} = \frac{500 \times 0.05}{0.6} = \frac{25}{0.6} \approx 41.67$$

์ด์ฒ˜๋Ÿผ ๋น„๊ต์  ํฐ ๋ˆ„์…€ ์ˆ˜๋Š” ์ด ์ƒํ™ฉ์—์„œ ๋Œ€๋ฅ˜๊ฐ€ ์ „๋„๋ฅผ ์••๋„ํ•˜๊ณ  ์žˆ์Œ์„ ํ™•์ธ์‹œ์ผœ ์ค๋‹ˆ๋‹ค.

์ž์ฃผ ๋ฌป๋Š” ์งˆ๋ฌธ

๋ˆ„์…€ ์ˆ˜๋Š” ํ•ญ์ƒ 1๋ณด๋‹ค ํฐ๊ฐ€์š”? ๋Œ€๋ฅ˜๊ฐ€ ์ผ์–ด๋‚˜๋Š” ์ƒํ™ฉ์—์„œ๋Š” ๊ทธ๋ ‡์Šต๋‹ˆ๋‹ค โ€” \(\text{Nu} \geq 1\)์ด๋ฉฐ, ๋Œ€๋ฅ˜๊ฐ€ ์•ฝํ•ด์ ธ ์ˆœ์ˆ˜ ์ „๋„์— ๊ฐ€๊นŒ์›Œ์งˆ์ˆ˜๋ก 1์— ๊ทผ์ ‘ํ•ฉ๋‹ˆ๋‹ค.

ํŠน์„ฑ ๊ธธ์ด๋ž€ ๋ฌด์—‡์ธ๊ฐ€์š”? ํ˜•์ƒ์— ๋”ฐ๋ผ ๋‹ฌ๋ผ์ง‘๋‹ˆ๋‹ค. ๊ด€ ๋‚ด๋ถ€ ์œ ๋™์—์„œ๋Š” ๊ด€์˜ ์ง๊ฒฝ, ํ‰ํŒ์—์„œ๋Š” ํ‰ํŒ์˜ ๊ธธ์ด, ๋น„์›ํ˜• ๋•ํŠธ์—์„œ๋Š” ์ˆ˜๋ ฅ ์ง๊ฒฝ์„ ์‚ฌ์šฉํ•ฉ๋‹ˆ๋‹ค.

๋ˆ„์…€ ์ˆ˜๋Š” ๋ ˆ์ด๋†€์ฆˆ ์ˆ˜, ํ”„๋ž€ํ‹€ ์ˆ˜์™€ ์–ด๋–ค ๊ด€๊ณ„๊ฐ€ ์žˆ๋‚˜์š”? \(\text{Nu} = 0.023 \cdot \text{Re}^{0.8} \cdot \text{Pr}^{0.4}\)(๋””ํˆฌ์Šค-๋ณผํ„ฐ ์‹)์™€ ๊ฐ™์€ ์‹คํ—˜์  ์ƒ๊ด€์‹์œผ๋กœ Nu๋ฅผ ์˜ˆ์ธกํ•˜๋Š” ๊ฒฝ์šฐ๊ฐ€ ๋งŽ์œผ๋ฉฐ, ์ด๋ ‡๊ฒŒ ๊ตฌํ•œ Nu๋Š” ๋‹ค์‹œ \(h = \frac{\text{Nu} \cdot k}{L}\) ๊ด€๊ณ„๋ฅผ ํ†ตํ•ด ์—ด์ „๋‹ฌ ๊ณ„์ˆ˜ h๋ฅผ ์‚ฐ์ถœํ•˜๋Š” ๋ฐ ์“ฐ์ž…๋‹ˆ๋‹ค.

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